CN110282643A - A kind of modified oxidized aluminum material and its preparation method and application - Google Patents
A kind of modified oxidized aluminum material and its preparation method and application Download PDFInfo
- Publication number
- CN110282643A CN110282643A CN201910631862.7A CN201910631862A CN110282643A CN 110282643 A CN110282643 A CN 110282643A CN 201910631862 A CN201910631862 A CN 201910631862A CN 110282643 A CN110282643 A CN 110282643A
- Authority
- CN
- China
- Prior art keywords
- solution
- rare earth
- nitrate
- earth nitrate
- preparation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000463 material Substances 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 31
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 29
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 239000000243 solution Substances 0.000 claims abstract description 151
- -1 rare earth nitrate Chemical class 0.000 claims abstract description 90
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract description 88
- 229910002651 NO3 Inorganic materials 0.000 claims abstract description 80
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 claims abstract description 36
- 229910001388 sodium aluminate Inorganic materials 0.000 claims abstract description 36
- 238000005406 washing Methods 0.000 claims abstract description 36
- 239000002270 dispersing agent Substances 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000006185 dispersion Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 20
- 230000032683 aging Effects 0.000 claims abstract description 18
- 239000007787 solid Substances 0.000 claims abstract description 17
- 239000002243 precursor Substances 0.000 claims abstract description 16
- 238000001556 precipitation Methods 0.000 claims abstract description 13
- 238000001914 filtration Methods 0.000 claims abstract description 10
- 229910001868 water Inorganic materials 0.000 claims abstract description 8
- 238000005507 spraying Methods 0.000 claims abstract description 7
- 238000001354 calcination Methods 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims abstract description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 48
- 238000011282 treatment Methods 0.000 claims description 30
- 238000003756 stirring Methods 0.000 claims description 26
- HSJPMRKMPBAUAU-UHFFFAOYSA-N cerium(3+);trinitrate Chemical compound [Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HSJPMRKMPBAUAU-UHFFFAOYSA-N 0.000 claims description 23
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 19
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 18
- 239000003054 catalyst Substances 0.000 claims description 17
- OERNJTNJEZOPIA-UHFFFAOYSA-N zirconium nitrate Chemical compound [Zr+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O OERNJTNJEZOPIA-UHFFFAOYSA-N 0.000 claims description 16
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 15
- 229910017604 nitric acid Inorganic materials 0.000 claims description 15
- 239000011259 mixed solution Substances 0.000 claims description 12
- IWOUKMZUPDVPGQ-UHFFFAOYSA-N barium nitrate Chemical compound [Ba+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O IWOUKMZUPDVPGQ-UHFFFAOYSA-N 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 9
- YWECOPREQNXXBZ-UHFFFAOYSA-N praseodymium(3+);trinitrate Chemical compound [Pr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O YWECOPREQNXXBZ-UHFFFAOYSA-N 0.000 claims description 7
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 6
- 239000000194 fatty acid Substances 0.000 claims description 6
- 229930195729 fatty acid Natural products 0.000 claims description 6
- CFYGEIAZMVFFDE-UHFFFAOYSA-N neodymium(3+);trinitrate Chemical compound [Nd+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O CFYGEIAZMVFFDE-UHFFFAOYSA-N 0.000 claims description 6
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 6
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 claims description 5
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 claims description 5
- 229920000053 polysorbate 80 Polymers 0.000 claims description 5
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims description 5
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims description 5
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims description 5
- QXPQVUQBEBHHQP-UHFFFAOYSA-N 5,6,7,8-tetrahydro-[1]benzothiolo[2,3-d]pyrimidin-4-amine Chemical compound C1CCCC2=C1SC1=C2C(N)=NC=N1 QXPQVUQBEBHHQP-UHFFFAOYSA-N 0.000 claims description 4
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims description 4
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 claims description 4
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 150000002148 esters Chemical class 0.000 claims description 2
- 150000004665 fatty acids Chemical class 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 8
- 239000007921 spray Substances 0.000 abstract description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 2
- 229910021529 ammonia Inorganic materials 0.000 abstract 1
- 239000006104 solid solution Substances 0.000 abstract 1
- 239000012153 distilled water Substances 0.000 description 14
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 12
- 230000003197 catalytic effect Effects 0.000 description 11
- 239000000706 filtrate Substances 0.000 description 11
- 239000011148 porous material Substances 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- 239000000047 product Substances 0.000 description 8
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000003837 high-temperature calcination Methods 0.000 description 3
- 150000002910 rare earth metals Chemical class 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052692 Dysprosium Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- KBQHZAAAGSGFKK-UHFFFAOYSA-N dysprosium atom Chemical compound [Dy] KBQHZAAAGSGFKK-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- JHJUUEHSAZXEEO-UHFFFAOYSA-M sodium;4-dodecylbenzenesulfonate Chemical compound [Na+].CCCCCCCCCCCCC1=CC=C(S([O-])(=O)=O)C=C1 JHJUUEHSAZXEEO-UHFFFAOYSA-M 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
- B01D53/945—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/021—After-treatment of oxides or hydroxides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/04—Preparation of alkali metal aluminates; Aluminium oxide or hydroxide therefrom
- C01F7/14—Aluminium oxide or hydroxide from alkali metal aluminates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明实施例涉及化学材料技术领域,具体涉及一种改性氧化铝材料及其制备方法和应用。The embodiments of the present invention relate to the technical field of chemical materials, in particular to a modified alumina material and its preparation method and application.
背景技术Background technique
随着社会的不断发展及经济的不断进步,汽车也逐渐成为人们出行必不可少的交通工具。中国家庭及人均的汽车保有量不断增多,而随着汽车保有量的增加,其大量排放到空气中的尾气则会带来较多的严重的环境问题,破坏城市的气候与环境,如大量雾霾及酸雨的形成等,而汽车尾气对大气环境的危害也会直接或间接地对人体的健康造成危害。With the continuous development of society and the continuous progress of economy, automobiles have gradually become an indispensable means of transportation for people to travel. The number of cars owned by Chinese families and per capita continues to increase, and with the increase in the number of cars, a large amount of exhaust gas emitted into the air will bring more serious environmental problems and damage the city's climate and environment, such as a large amount of fog The formation of haze and acid rain, etc., and the harm of automobile exhaust to the atmospheric environment will also directly or indirectly cause harm to human health.
三元催化净化技术是将一种填充了粉体催化剂的蜂窝状陶瓷安装在发动机的下游从而对发动机产生的尾气进行净化的技术。汽油通过在发动机中燃烧后,主要会产生一氧化碳,氮氧化物,碳氢化合物以及微粒等污染物,尾气经过三元催化系统,其中的一氧化碳,碳氧化合物,氮氧化物会受到催化剂的催化从而反应生成水,二氧化碳以及氮气等无害物质,其中粉体催化剂的性能决定了三元催化系统的净化能力。The three-way catalytic purification technology is a technology that installs a honeycomb ceramic filled with powder catalyst in the downstream of the engine to purify the exhaust gas generated by the engine. After gasoline is burned in the engine, it will mainly produce pollutants such as carbon monoxide, nitrogen oxides, hydrocarbons, and particulates. The exhaust gas passes through the three-way catalytic system, and the carbon monoxide, carbon oxides, and nitrogen oxides will be catalyzed by the catalyst. The reaction produces harmless substances such as water, carbon dioxide and nitrogen, among which the performance of the powder catalyst determines the purification ability of the three-way catalytic system.
催化剂主要包括贵金属催化剂,催化助剂,稳定剂以及γ-Al2O3涂层材料,其中γ-Al2O3为三元催化剂提供了较大的表面积,是催化剂与尾气充分接触,从而保证催化效率;但γ-Al2O3在温度瞬态达到800℃时,其结构转变为α-Al2O3,比表面积、孔容、储放氧能力下降,从而使催化效率下降,由于三元催化器位置接近汽车发动机,其工作温度最高可达到1000℃以上,故通常的氧化铝无法作为三元催化器中的催化剂载体。Catalysts mainly include noble metal catalysts, catalytic promoters, stabilizers and γ-Al 2 O 3 coating materials, among which γ-Al 2 O 3 provides a larger surface area for the three-way catalyst, which ensures full contact between the catalyst and the exhaust gas, thus ensuring Catalytic efficiency; but when the temperature of γ-Al 2 O 3 reaches 800°C in a transient state, its structure transforms into α-Al 2 O 3 , and the specific surface area, pore volume, and oxygen storage and release capacity decrease, thereby reducing the catalytic efficiency. The position of the primary catalyst is close to the automobile engine, and its operating temperature can reach above 1000°C, so ordinary alumina cannot be used as the catalyst carrier in the three-way catalytic converter.
发明内容Contents of the invention
为此,本发明实施例第一目的提供一种改性氧化铝材料,该改性氧化铝材料在高于800℃的条件下,具有优异的比表面积和孔容,解决了现有技术中氧化铝材料在高于800℃时,比表面积、孔容、储放氧能力下降的问题。For this reason, the first purpose of the embodiment of the present invention is to provide a modified alumina material, which has excellent specific surface area and pore volume at a temperature higher than 800°C, and solves the problem of oxidation in the prior art. When the aluminum material is higher than 800°C, the specific surface area, pore volume, and oxygen storage and release capacity decrease.
本发明实施例第二目的提供一种改性氧化铝材料的制备方法,该制备方法采用设备比较简单、易于操作,并采用多种稀土元素进行改性,并通过高温煅烧处理,使得制备得到的改性氧化铝材料具有优异的热稳定性、比表面积和孔容。The second purpose of the embodiments of the present invention is to provide a method for preparing a modified alumina material. The preparation method uses relatively simple equipment and is easy to operate, and uses various rare earth elements for modification, and high-temperature calcination treatment, so that the prepared Modified alumina materials have excellent thermal stability, specific surface area and pore volume.
本发明实施例的第三目的提供一种改性氧化铝材料在汽车尾气催化剂载体中的应用,该应用能够使得催化剂载体在高于800℃下,具有优异的比表面积、孔容、储放氧性能,能够有效提高催化剂载体的耐用性和催化效率。The third purpose of the embodiment of the present invention is to provide an application of a modified alumina material in an automobile exhaust catalyst carrier. performance, which can effectively improve the durability and catalytic efficiency of the catalyst carrier.
为了实现上述目的,本发明实施例提供如下技术方案:In order to achieve the above purpose, embodiments of the present invention provide the following technical solutions:
根据本发明实施例的第一方面提供一种改性氧化铝材料的制备方法,所述制备方法包括如下步骤:According to the first aspect of the embodiments of the present invention, there is provided a method for preparing a modified alumina material, the preparation method comprising the following steps:
(a)将铝酸钠溶液和稀土硝酸盐溶液喷淋到分散剂溶液中,得到混合液;(a) spraying the sodium aluminate solution and the rare earth nitrate solution into the dispersant solution to obtain a mixed solution;
(b)将混合液进行沉淀处理、老化处理、过滤、洗涤,得到前驱体;(b) subjecting the mixed solution to precipitation treatment, aging treatment, filtration and washing to obtain a precursor;
(c)将稀土硝酸盐溶液和氨水喷淋至分散液中并进行沉淀处理、老化处理、过滤、洗涤,得到固态物;(c) spraying the rare earth nitrate solution and ammonia water into the dispersion liquid and performing precipitation treatment, aging treatment, filtering and washing to obtain a solid;
(d)将前驱体和固态物分别溶于热水中,并将固态物溶液喷淋至前驱体溶液中并进行搅拌,待搅拌结束进行老化处理、过滤、烘干、煅烧、粉碎,得到所述改性氧化铝材料。(d) Dissolving the precursor and the solid matter in hot water respectively, and spraying the solid matter solution into the precursor solution and stirring, after the stirring is completed, carry out aging treatment, filtration, drying, calcination, and pulverization to obtain the obtained The modified alumina material described above.
本发明上述制备方法采用设备比较简单、易于操作,并采用多种稀土元素进行改性,并通过高温煅烧处理,使得制备得到的改性氧化铝材料具有优异的热稳定性、比表面积和孔容。The above-mentioned preparation method of the present invention adopts relatively simple equipment, is easy to operate, and uses various rare earth elements for modification, and undergoes high-temperature calcination treatment, so that the prepared modified alumina material has excellent thermal stability, specific surface area and pore volume .
进一步地,所述步骤(a)中,铝酸钠溶液和稀土硝酸盐溶液体积比为1∶(0.8-1.2);铝酸钠溶液浓度为50-150g/L;稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的1-40%,稀土硝酸盐溶液中溶剂为质量分数为15-80%的硝酸溶液;稀土硝酸盐溶液中稀土硝酸盐选自硝酸镧、硝酸铈、硝酸锆、硝酸镨、硝酸钕、硝酸钡和硝酸镝中的任意二种或多种。通过对铝酸钠溶液浓度的限定,能够保障制备改性氧化铝材料的粒径,并通过稀土硝酸盐种类及多种选择,能够提高改性氧化铝材料的整体性能。Further, in the step (a), the volume ratio of the sodium aluminate solution and the rare earth nitrate solution is 1: (0.8-1.2); the concentration of the sodium aluminate solution is 50-150g/L; the rare earth nitric acid in the rare earth nitrate solution The quality of the salt is 1-40% of the aluminum mass calculated as alumina in the sodium aluminate solution, and the solvent in the rare earth nitrate solution is a nitric acid solution with a mass fraction of 15-80%; the rare earth nitrate in the rare earth nitrate solution is selected from nitric acid Any two or more of lanthanum, cerium nitrate, zirconium nitrate, praseodymium nitrate, neodymium nitrate, barium nitrate and dysprosium nitrate. By limiting the concentration of the sodium aluminate solution, the particle size of the modified alumina material can be guaranteed, and the overall performance of the modified alumina material can be improved by the type and selection of rare earth nitrates.
进一步地,所述步骤(a)中,铝酸钠溶液和稀土硝酸盐溶液的总体积与分散剂溶液的体积比为15∶(2-3);分散剂溶液中分散剂选自PEG-2000、十二烷基苯磺酸钠、聚乙烯吡咯烷酮、吐温80、聚乙二醇脂肪酸酯和脂肪酸聚氧乙烯酯中的任意一种或多种;分散剂溶液中分散剂的质量为铝酸钠溶液中以氧化铝计铝质量的0.1-10%。通过上述限定,能够更好的提高制备改性氧化铝材料的比表面积和孔容。Further, in the step (a), the volume ratio of the total volume of the sodium aluminate solution and the rare earth nitrate solution to the dispersant solution is 15: (2-3); the dispersant in the dispersant solution is selected from PEG-2000 , sodium dodecylbenzenesulfonate, polyvinylpyrrolidone, Tween 80, polyethylene glycol fatty acid ester and fatty acid polyoxyethylene ester; the quality of the dispersant in the dispersant solution is aluminum 0.1-10% of the mass of aluminum calculated as alumina in the sodium bicarbonate solution. Through the above definition, the specific surface area and pore volume of the prepared modified alumina material can be better improved.
进一步地,所述步骤(b)中,沉淀处理为在搅拌条件下,控制混合液温度为40-90℃,pH值为6.5-8.5;老化处理为在65-95℃下老化1-100h。通过上述处理,能够提高制备改性氧化铝材料的高温热稳定性、比表面积和孔容。Further, in the step (b), the precipitation treatment is to control the temperature of the mixed solution at 40-90° C. and the pH value to 6.5-8.5 under stirring conditions; the aging treatment is to age at 65-95° C. for 1-100 h. Through the above treatment, the high temperature thermal stability, specific surface area and pore volume of the prepared modified alumina material can be improved.
进一步地,所述步骤(c)中,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的15-25%,稀土硝酸盐溶液中溶剂为质量分数为15-80%的硝酸溶液,稀土硝酸盐溶液的质量浓度为250-350g/L,稀土硝酸盐溶液中稀土硝酸盐选自硝酸镧、硝酸铈、硝酸锆、硝酸镨、硝酸钕、硝酸钡和硝酸镝中的任意二种或多种;优选地,当稀土硝酸盐溶液中含有硝酸铈时,先将硝酸铈溶于硝酸溶液中,并在稀土硝酸铈溶液中添加双氧水并搅拌混匀,其中双氧水的的质量浓度为30%,双氧水添加量为稀土硝酸盐溶液体积的15-18%;搅拌时间为25-35min;随后再将其他稀土硝酸盐置入稀土硝酸铈溶液中配的相应浓度的稀土硝酸盐溶液。Further, in the step (c), the quality of the rare earth nitrate in the rare earth nitrate solution is 15-25% of the aluminum mass in the sodium aluminate solution, and the mass fraction of the solvent in the rare earth nitrate solution is 15% -80% nitric acid solution, the mass concentration of the rare earth nitrate solution is 250-350g/L, and the rare earth nitrate in the rare earth nitrate solution is selected from lanthanum nitrate, cerium nitrate, zirconium nitrate, praseodymium nitrate, neodymium nitrate, barium nitrate and nitric acid Any two or more of dysprosium; preferably, when the rare earth nitrate solution contains cerium nitrate, the cerium nitrate is first dissolved in the nitric acid solution, and hydrogen peroxide is added to the rare earth cerium nitrate solution and stirred well, wherein the hydrogen peroxide The mass concentration of hydrogen peroxide is 30%, and the amount of hydrogen peroxide added is 15-18% of the volume of the rare earth nitrate solution; the stirring time is 25-35min; Nitrate solution.
进一步地,所述步骤(c)中,稀土硝酸盐溶液、氨水和分散液的体积比为(5-7)∶(5-7)∶(4-6);氨水的质量浓度为45-55%;分散液中的溶质选自PEG-2000、十二烷基苯磺酸钠、聚乙烯吡咯烷酮、吐温80、聚乙二醇脂肪酸酯和脂肪酸聚氧乙烯酯中的任意一种或多种;分散液中的溶质的质量为铝酸钠溶液中以氧化铝计铝质量的4-6%。Further, in the step (c), the volume ratio of the rare earth nitrate solution, ammonia water and dispersion liquid is (5-7): (5-7): (4-6); the mass concentration of ammonia water is 45-55 %; the solute in the dispersion is selected from any one or more of PEG-2000, sodium dodecylbenzenesulfonate, polyvinylpyrrolidone, Tween 80, polyethylene glycol fatty acid ester and polyoxyethylene fatty acid ester species; the mass of the solute in the dispersion liquid is 4-6% of the mass of aluminum calculated as alumina in the sodium aluminate solution.
进一步地,所述步骤(c)中,沉淀处理为在搅拌条件下,调节pH值至8.5-9.0;老化处理为在70-80℃下老化20-26h。Further, in the step (c), the precipitation treatment is to adjust the pH value to 8.5-9.0 under stirring conditions; the aging treatment is to age at 70-80° C. for 20-26 hours.
进一步地,所述步骤(d)中,搅拌温度为75-85℃,搅拌时间为3-5h;老化处理为在70-80℃下老化20-28h;烘干温度为85-95℃;煅烧温度为800-1000℃,时间为2-10h;粉碎为采用球磨机进行粉碎至25-35μm;热水温度为85-95℃。本发明通过煅烧处理,能够提高制备改性氧化铝材料的热稳定性。Further, in the step (d), the stirring temperature is 75-85°C, and the stirring time is 3-5h; the aging treatment is aging at 70-80°C for 20-28h; the drying temperature is 85-95°C; The temperature is 800-1000°C, and the time is 2-10h; the pulverization is carried out by a ball mill to 25-35 μm; the temperature of the hot water is 85-95°C. The invention can improve the thermal stability of the prepared modified alumina material through calcining treatment.
进一步地,所述步骤(b)和(c)中,洗涤为采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至8.0-10.0;蒸馏水与过滤物的固液比为(9-15):1,洗涤温度为60-95℃,洗涤时间为10-60min,洗涤次数为3-5次。Further, in the steps (b) and (c), the washing is to use distilled water to wash the filtrate, and add ammonia water during the washing process to adjust the pH to 8.0-10.0; the solid-liquid ratio of distilled water to the filtrate is (9-15 ): 1. The washing temperature is 60-95°C, the washing time is 10-60min, and the washing times are 3-5 times.
本发明通过洗涤处理能够减少制备产物中的杂质,并能够进行脱钠,可进一步提高制备改性氧化铝材料的活性。The invention can reduce the impurities in the prepared product through washing treatment, and can perform sodium removal, and can further improve the activity of preparing the modified alumina material.
根据本发明实施例的第二方面提供他一种改性氧化铝材料,所述改性氧化铝材料由上述制备方法制备得到。According to the second aspect of the embodiments of the present invention, there is provided a modified alumina material prepared by the above preparation method.
本发明上述改性氧化铝材料具有优异的热稳定性、比表面积、孔容以及储放氧性能。The above-mentioned modified alumina material of the present invention has excellent thermal stability, specific surface area, pore volume and oxygen storage and release performance.
本发明实施例第三方面提供一种上述改性氧化铝材料在汽车尾气催化剂载体中的应用。通过将上述改性氧化铝材料作为催化剂载体,能够提高催化剂载体的使用寿命,并提高催化效率。The third aspect of the embodiment of the present invention provides an application of the above-mentioned modified alumina material in a carrier of an automobile exhaust catalyst. By using the above-mentioned modified alumina material as a catalyst carrier, the service life of the catalyst carrier can be increased and the catalytic efficiency can be improved.
本发明实施例具有如下优点:Embodiments of the present invention have the following advantages:
(1)本发明制备方法采用设备比较简单、易于操作,并采用多种稀土元素进行改性,并通过高温煅烧处理,能够提高制备产品的综合性能。(1) The preparation method of the present invention adopts relatively simple equipment, is easy to operate, uses various rare earth elements for modification, and performs high-temperature calcination treatment to improve the comprehensive performance of the prepared product.
(2)本发明改性氧化铝材料具有优异的热稳定性、比表面积、孔容以及储放氧性能。(2) The modified alumina material of the present invention has excellent thermal stability, specific surface area, pore volume and oxygen storage and release performance.
(3)本发明通过将改性氧化铝材料作为催化剂载体,能够提高催化剂载体的使用寿命,并提高催化效率。(3) The present invention can improve the service life of the catalyst carrier and improve the catalytic efficiency by using the modified alumina material as the catalyst carrier.
具体实施方式Detailed ways
以下由特定的具体实施例说明本发明的实施方式,熟悉此技术的人士可由本说明书所揭露的内容轻易地了解本发明的其他优点及功效,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The implementation mode of the present invention is illustrated by specific specific examples below, and those who are familiar with this technology can easily understand other advantages and effects of the present invention from the contents disclosed in this description. Obviously, the described embodiments are a part of the present invention. , but not all examples. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例1Example 1
本实施例为一种改性氧化铝材料的制备方法,所述制备方法包括如下步骤:This embodiment is a preparation method of a modified alumina material, and the preparation method includes the following steps:
(a)将浓度为50g/L铝酸钠溶液和稀土硝酸盐溶液喷淋到分散剂溶液中,得到混合液,其中铝酸钠溶液和稀土硝酸盐溶液的体积比为1∶0.8,铝酸钠溶液和稀土硝酸盐溶液的总体积与分散剂溶液的体积比为15∶2,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的1%,稀土硝酸盐溶液中溶剂为质量分数为15%的硝酸溶液;稀土硝酸盐溶液中稀土硝酸盐为硝酸镧和硝酸镝,分散剂溶液中分散剂为聚乙烯吡咯烷酮和吐温80;分散剂溶液中分散剂的质量为铝酸钠溶液中以氧化铝计铝质量的0.1%;(a) Spray the sodium aluminate solution and the rare earth nitrate solution with a concentration of 50g/L into the dispersant solution to obtain a mixed solution, wherein the volume ratio of the sodium aluminate solution and the rare earth nitrate solution is 1:0.8, and the aluminum acid The volume ratio of the total volume of the sodium solution and the rare earth nitrate solution to the dispersant solution is 15:2, the quality of the rare earth nitrate in the rare earth nitrate solution is 1% of the aluminum mass calculated as aluminum oxide in the sodium aluminate solution, and the rare earth nitric acid The solvent in the salt solution is a nitric acid solution with a mass fraction of 15%; the rare earth nitrate in the rare earth nitrate solution is lanthanum nitrate and dysprosium nitrate, and the dispersant in the dispersant solution is polyvinylpyrrolidone and Tween 80; the dispersant in the dispersant solution The mass is 0.1% of the mass of aluminum calculated as alumina in the sodium aluminate solution;
(b)将混合液在40℃、pH6.5-8.5以及搅拌条件下进行沉淀处理,随后在95℃下老化1h、过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至8.0,蒸馏水与过滤物的固液比为9∶1,洗涤温度为60℃,洗涤时间为60min,洗涤次数为3次,得到前驱体;(b) Precipitate the mixed solution at 40°C, pH 6.5-8.5 and stirring conditions, then age at 95°C for 1 hour, filter, and then wash the filtrate with distilled water. During the washing process, add ammonia water to adjust the pH to 8.0, the solid-to-liquid ratio of distilled water to filtrate is 9:1, the washing temperature is 60°C, the washing time is 60min, and the washing times are 3 times to obtain the precursor;
(c)按照浓度为350g/L的稀土硝酸盐溶液、浓度为45%氨水和分散液的体积比为5∶7∶4,将稀土硝酸盐溶液和氨水喷淋至分散液中并在pH8.5-9.0、搅拌条件下进行沉淀处理,随后在70℃下老化26h,然后过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至8.0,蒸馏水与过滤物的固液比为9∶1,洗涤温度为60℃,洗涤时间为60min,洗涤次数为3次,得到固态物,其中分散液中的溶质为聚乙烯吡咯烷酮和吐温80;分散液中的溶质的质量为铝酸钠溶液中以氧化铝计铝质量的4%,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的15%,稀土硝酸盐溶液中溶剂为质量分数为15%的硝酸溶液,稀土硝酸盐溶液中稀土硝酸盐为硝酸锆和硝酸镨;(c) according to concentration is the rare earth nitrate solution of 350g/L, concentration is that the volume ratio of 45% ammonia water and dispersion liquid is 5:7:4, rare earth nitrate solution and ammonia water are sprayed in the dispersion liquid and at pH8. 5-9.0, carry out precipitation treatment under stirring conditions, then age at 70°C for 26 hours, then filter, and then use distilled water to wash the filtrate, add ammonia water during the washing process to adjust the pH to 8.0, the solid-liquid ratio of distilled water and filtrate is 9:1, the washing temperature is 60°C, the washing time is 60min, and the number of washings is 3 times to obtain a solid, wherein the solute in the dispersion is polyvinylpyrrolidone and Tween 80; the mass of the solute in the dispersion is alumina 4% of the aluminum mass in the sodium solution, the mass fraction of the rare earth nitrate in the rare earth nitrate solution is 15% of the aluminum mass in the sodium aluminate solution, and the mass fraction of the solvent in the rare earth nitrate solution is 15% % nitric acid solution, the rare earth nitrate in the rare earth nitrate solution is zirconium nitrate and praseodymium nitrate;
(d)将前驱体和固态物分别溶于95℃的热水中,并将固态物溶液喷淋至前驱体溶液中并在75℃下进行搅拌3h,待搅拌结束在80℃下老化20h,然后过滤,并在85℃下烘干,再在800℃煅烧10h,采用球磨机进行粉碎至25-35μm,得到改性氧化铝材料。(d) Dissolve the precursor and solid matter in hot water at 95°C respectively, spray the solid matter solution into the precursor solution and stir at 75°C for 3h, and age at 80°C for 20h after the stirring is completed, Then filter and dry at 85°C, then calcined at 800°C for 10 hours, and pulverize to 25-35μm with a ball mill to obtain a modified alumina material.
实施例2Example 2
本实施例为一种改性氧化铝材料的制备方法,所述制备方法包括如下步骤:This embodiment is a preparation method of a modified alumina material, and the preparation method includes the following steps:
(a)将浓度为150g/L铝酸钠溶液和稀土硝酸盐溶液喷淋到分散剂溶液中,得到混合液,其中铝酸钠溶液和稀土硝酸盐溶液按照的体积比为1∶1.2,铝酸钠溶液和稀土硝酸盐溶液的总体积与分散剂溶液的体积比为5∶1,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的40%,稀土硝酸盐溶液中溶剂为质量分数为80%的硝酸溶液;稀土硝酸盐溶液中稀土硝酸盐选自硝酸镧、硝酸铈和硝酸锆,分散剂溶液中分散剂为PEG-2000和十二烷基苯磺酸钠;分散剂溶液中分散剂的质量为铝酸钠溶液中以氧化铝计铝质量的10%;(a) Spray the sodium aluminate solution and the rare earth nitrate solution with a concentration of 150g/L into the dispersant solution to obtain a mixed solution, wherein the sodium aluminate solution and the rare earth nitrate solution are in a volume ratio of 1:1.2, and the aluminum The volume ratio of the total volume of the sodium aluminate solution and the rare earth nitrate solution to the dispersant solution is 5: 1, and the quality of the rare earth nitrate in the rare earth nitrate solution is 40% of the aluminum mass in the sodium aluminate solution calculated as aluminum oxide. The solvent in the nitrate solution is nitric acid solution with a mass fraction of 80%; the rare earth nitrate in the rare earth nitrate solution is selected from lanthanum nitrate, cerium nitrate and zirconium nitrate, and the dispersant in the dispersant solution is PEG-2000 and dodecylbenzene Sodium sulfonate; the quality of the dispersant in the dispersant solution is 10% of the aluminum quality calculated as aluminum oxide in the sodium aluminate solution;
(b)将混合液在90℃、pH6.5-8.5以及搅拌条件下进行沉淀处理,随后在65℃下老化100h、过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至10,蒸馏水与过滤物的固液比为15∶1,洗涤温度为95℃,洗涤时间为10min,洗涤次数为5次,得到前驱体;(b) Precipitate the mixed solution at 90°C, pH6.5-8.5 and stirring conditions, then age at 65°C for 100h, filter, and then wash the filtrate with distilled water, add ammonia water during the washing process to adjust the pH to 10. The solid-to-liquid ratio of distilled water to filtrate is 15:1, the washing temperature is 95°C, the washing time is 10 min, and the washing times are 5 times to obtain the precursor;
(c)按照浓度为250g/L的稀土硝酸盐溶液、浓度为55%氨水和分散液的体积比为7∶5∶6,将稀土硝酸盐溶液和氨水喷淋至分散液中并在pH8.5-9.0、搅拌条件下进行沉淀处理,随后在80℃下老化20h,然后过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至10,蒸馏水与过滤的固液比为15∶1,洗涤温度为95℃,洗涤时间为10min,洗涤次数为5次,得到固态物,其中分散液中的溶质为PEG-2000和十二烷基苯磺酸钠;分散液中的溶质的质量为铝酸钠溶液中以氧化铝计铝质量的6%,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的25%,稀土硝酸盐溶液中溶剂为质量分数为80%的硝酸溶液,稀土硝酸盐溶液中稀土硝酸盐为硝酸钕和硝酸钡;(c) according to concentration is the rare earth nitrate solution of 250g/L, concentration is that the volume ratio of 55% ammonia water and dispersion liquid is 7:5:6, rare earth nitrate solution and ammonia water are sprayed in the dispersion liquid and at pH8. 5-9.0. Precipitate under stirring conditions, then age at 80°C for 20 hours, then filter, and then wash the filtrate with distilled water. During the washing process, add ammonia water to adjust the pH to 10. The solid-to-liquid ratio of distilled water and filtration is 15. : 1, the washing temperature is 95°C, the washing time is 10min, and the number of times of washing is 5 times to obtain a solid, wherein the solute in the dispersion is PEG-2000 and sodium dodecylbenzenesulfonate; The quality is 6% of the aluminum mass calculated as alumina in the sodium aluminate solution, the quality of the rare earth nitrate in the rare earth nitrate solution is 25% of the aluminum mass calculated as alumina in the sodium aluminate solution, and the solvent in the rare earth nitrate solution is A nitric acid solution with a mass fraction of 80%, and the rare earth nitrates in the rare earth nitrate solution are neodymium nitrate and barium nitrate;
(d)将前驱体和固态物分别溶于85℃的热水中,并将固态物溶液喷淋至前驱体溶液中并在85℃下进行搅拌5h,待搅拌结束在70℃下老化28h,然后过滤,并在95℃下烘干,再在1000℃煅烧2h,采用球磨机进行粉碎至25-35μm,得到改性氧化铝材料。(d) Dissolve the precursor and solid matter in hot water at 85°C respectively, spray the solid matter solution into the precursor solution and stir at 85°C for 5h, and age at 70°C for 28h after the stirring is completed, Then filter and dry at 95°C, then calcined at 1000°C for 2 hours, and pulverize to 25-35μm with a ball mill to obtain a modified alumina material.
实施例3Example 3
本实施例为一种改性氧化铝材料的制备方法,所述制备方法包括如下步骤:This embodiment is a preparation method of a modified alumina material, and the preparation method includes the following steps:
(a)将浓度为100g/L铝酸钠溶液和稀土硝酸盐溶液喷淋到分散剂溶液中,得到混合液,其中铝酸钠溶液和稀土硝酸盐溶液按照的体积比为1∶1,铝酸钠溶液和稀土硝酸盐溶液的总体积与分散剂溶液的体积比为6∶1,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的3%,稀土硝酸盐溶液中溶剂为质量分数为65%的硝酸溶液;稀土硝酸盐溶液中稀土硝酸盐为硝酸镨和硝酸钕,分散剂溶液中分散剂为PEG-2000溶液;分散剂溶液中分散剂的质量为铝酸钠溶液中以氧化铝计铝质量的5%;(a) Spray the sodium aluminate solution and the rare earth nitrate solution with a concentration of 100g/L into the dispersant solution to obtain a mixed solution, wherein the sodium aluminate solution and the rare earth nitrate solution are in a volume ratio of 1:1, and the aluminum The volume ratio of the total volume of the sodium aluminate solution and the rare earth nitrate solution to the dispersant solution is 6:1, and the quality of the rare earth nitrate in the rare earth nitrate solution is 3% of the aluminum mass in the sodium aluminate solution calculated as aluminum oxide. The solvent in the nitrate solution is a nitric acid solution with a mass fraction of 65%; the rare earth nitrate in the rare earth nitrate solution is praseodymium nitrate and neodymium nitrate, and the dispersant in the dispersant solution is PEG-2000 solution; the quality of the dispersant in the dispersant solution It is 5% of the mass of aluminum calculated as alumina in sodium aluminate solution;
(b)将混合液在80℃、pH7.0-7.5以及搅拌条件下进行沉淀处理,随后在90℃下老化40h、过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至9,蒸馏水与过滤的固液比为12∶1,洗涤温度为75℃,洗涤时间为40min,洗涤次数为4次,得到前驱体;(b) Precipitate the mixed solution at 80°C, pH7.0-7.5 and stirring conditions, then age at 90°C for 40h, filter, and then wash the filtrate with distilled water, add ammonia water during the washing process to adjust the pH to 9. The solid-to-liquid ratio of distilled water to filtration is 12:1, the washing temperature is 75°C, the washing time is 40 min, and the washing times are 4 times to obtain the precursor;
(c)将硝酸铈溶于浓度为65%的硝酸溶液中,并在稀土硝酸铈溶液中添加质量浓度为30%双氧水并搅拌30min混匀,随后再将硝酸锆置入稀土硝酸铈溶液中配的浓度为300g/L的稀土硝酸盐溶液,稀土硝酸盐溶液中稀土硝酸盐的质量为铝酸钠溶液中以氧化铝计铝质量的18%,且硝酸铈和硝酸锆质量比为5∶4;双氧水添加量为稀土硝酸盐溶液体积的17%;随后,按照稀土硝酸盐溶液、浓度为50%的氨水和分散液的体积比为6∶6∶5,将稀土硝酸盐溶液和氨水喷淋至分散液中并在pH8.5-9.0、搅拌条件下进行沉淀处理,随后在75℃下老化24h,然后过滤,再采用蒸馏水对过滤物进行洗涤,洗涤过程中加入氨水调节pH至9,蒸馏水与过滤的固液比为12∶1,洗涤温度为75℃,洗涤时间为40min,洗涤次数为4次,得到固态物;分散液中的溶质为PEG-2000;分散液中的溶质的质量为铝酸钠溶液中以氧化铝计铝质量的5%;(c) Dissolve cerium nitrate in a nitric acid solution with a concentration of 65%, and add 30% hydrogen peroxide with a mass concentration of 30% in the rare earth cerium nitrate solution and stir for 30 minutes to mix evenly, then put the zirconium nitrate into the rare earth cerium nitrate solution to prepare The concentration of the rare earth nitrate solution is 300g/L, the quality of the rare earth nitrate in the rare earth nitrate solution is 18% of the aluminum mass calculated as aluminum oxide in the sodium aluminate solution, and the mass ratio of cerium nitrate and zirconium nitrate is 5:4 The amount of hydrogen peroxide added is 17% of the volume of the rare earth nitrate solution; subsequently, according to the volume ratio of the rare earth nitrate solution, the concentration of 50% ammonia water and the dispersion liquid is 6:6:5, the rare earth nitrate solution and ammonia water are sprayed Put it into the dispersion liquid and carry out precipitation treatment under the condition of pH 8.5-9.0 under stirring, then aging at 75°C for 24 hours, then filter, and then wash the filtrate with distilled water, add ammonia water during the washing process to adjust the pH to 9, distilled water The solid-liquid ratio with filtration is 12:1, the washing temperature is 75°C, the washing time is 40min, and the number of washings is 4 times to obtain a solid; the solute in the dispersion is PEG-2000; the mass of the solute in the dispersion is 5% of the mass of aluminum calculated as alumina in the sodium aluminate solution;
(d)将前驱体和固态物分别溶于90℃的热水中,并将固态物溶液喷淋至前驱体溶液中并在80℃下进行搅拌4h,待搅拌结束在75℃下老化24h,然后过滤,并在90℃下烘干,再在900℃煅烧6h,采用球磨机进行粉碎至25-35μm,得到改性氧化铝材料。(d) Dissolve the precursor and solid matter in hot water at 90°C respectively, spray the solid matter solution into the precursor solution and stir at 80°C for 4 hours, and age at 75°C for 24 hours after the stirring is completed, Then filter, dry at 90°C, calcined at 900°C for 6 hours, and pulverize to 25-35μm with a ball mill to obtain a modified alumina material.
对照例1Comparative example 1
本对照例为一种改性氧化铝材料的制备方法,该制备方法与实施例3中的制备方法基本相同,区别仅在于步骤(a)中稀土硝酸盐溶液为硝酸镨溶液;步骤(c)中稀土硝酸盐溶液为硝酸铈水溶液。This comparative example is a preparation method of a modified alumina material, which is basically the same as the preparation method in Example 3, except that the rare earth nitrate solution in step (a) is a praseodymium nitrate solution; step (c) The medium rare earth nitrate solution is an aqueous solution of cerium nitrate.
对照例2Comparative example 2
本对照例为一种改性氧化铝材料的制备方法,该制备方法与实施例3中的制备方法基本相同,区别仅在于步骤(b)和步骤(c)中的沉淀处理过程中未控制pH值。This comparative example is a preparation method of a modified alumina material, the preparation method is basically the same as the preparation method in Example 3, the only difference is that the pH is not controlled during the precipitation treatment in step (b) and step (c) value.
对照例3Comparative example 3
本对照例为一种改性氧化铝材料的制备方法,该制备方法与实施例3中的制备方法基本相同,区别仅在于步骤(b)和步骤(c)中未进行洗涤处理。This comparative example is a preparation method of a modified alumina material, which is basically the same as the preparation method in Example 3, except that no washing treatment is performed in step (b) and step (c).
对照例4Comparative example 4
本对照例为现有三元催化系统中采用的γ-Al2O3涂层材料,该涂层材料为Sasol厂家生产得产品编号为PURALOX SCFa-140L3的涂层材料。This comparative example is the γ-Al 2 O 3 coating material used in the existing three-way catalytic system. The coating material is the coating material with the product number PURALOX SCFa-140L3 produced by Sasol manufacturer.
实验例1Experimental example 1
选取上述实施例1-3和对照例1-4中制备得到的改性氧化铝材料;Select the modified alumina material prepared in the above-mentioned Examples 1-3 and Comparative Examples 1-4;
分别采用氮吸附法和透射电镜法对上述各材料的新鲜态及900℃煅烧4h后的表面积、孔容、γ-Al2O3的含量进行检测,检测结果如表1所示:The surface area, pore volume, and content of γ-Al 2 O 3 of the above-mentioned materials in fresh state and after calcination at 900°C for 4 hours were detected by nitrogen adsorption method and transmission electron microscope respectively. The detection results are shown in Table 1:
表1Table 1
由表1可知:It can be seen from Table 1 that:
本发明实施例制备得到的稀土复合改性氧化铝具有优异的热稳定性,能够在900℃下,使得产品具有优异的比表面积、孔容和较高的γ-Al2O3含量;然而对照例中改变本申请制备方法及其原料,导致了制备产品在高温下性能的降低,影响产品性能;通过与对照例4相比较,本发明实施例制备得到的产品达到了和产品编号为PURALOX SCFa-140L3的涂层材料相当的性能。The rare earth composite modified alumina prepared in the embodiment of the present invention has excellent thermal stability, and can make the product have excellent specific surface area, pore volume and high γ-Al 2 O 3 content at 900°C; however, the control In the example, changing the preparation method of the present application and its raw materials has caused the reduction of the performance of the prepared product at high temperature, which affects the product performance; by comparing with the comparative example 4, the product prepared by the embodiment of the present invention has reached the product number of PURALOX SCFa -140L3 coating material comparable performance.
虽然,上文中已经用一般性说明及具体实施例对本发明作了详尽的描述,但在本发明基础上,可以对之作一些修改或改进,这对本领域技术人员而言是显而易见的。因此,在不偏离本发明精神的基础上所做的这些修改或改进,均属于本发明要求保护的范围。Although the present invention has been described in detail with general descriptions and specific examples above, it is obvious to those skilled in the art that some modifications or improvements can be made on the basis of the present invention. Therefore, the modifications or improvements made on the basis of not departing from the spirit of the present invention all belong to the protection scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910631862.7A CN110282643A (en) | 2019-07-12 | 2019-07-12 | A kind of modified oxidized aluminum material and its preparation method and application |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910631862.7A CN110282643A (en) | 2019-07-12 | 2019-07-12 | A kind of modified oxidized aluminum material and its preparation method and application |
Publications (1)
Publication Number | Publication Date |
---|---|
CN110282643A true CN110282643A (en) | 2019-09-27 |
Family
ID=68022830
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910631862.7A Pending CN110282643A (en) | 2019-07-12 | 2019-07-12 | A kind of modified oxidized aluminum material and its preparation method and application |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110282643A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113337107A (en) * | 2021-05-29 | 2021-09-03 | 巢湖市龙鑫塑料有限公司 | Method for composite modification of nylon 6 by nano-alumina |
CN115228434A (en) * | 2022-07-21 | 2022-10-25 | 南京信息工程大学 | Surface-wrapped gamma-Al 2 O 3 : carbon nanotube adsorbent with Dy & lt 3+ & gt particles and preparation method thereof |
CN116332224A (en) * | 2023-03-22 | 2023-06-27 | 广东长信精密设备有限公司 | Spherical gallium oxide and preparation process thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090023581A1 (en) * | 2004-12-30 | 2009-01-22 | Magnesium Elektron Limited | THERMALLY STABLE DOPED AND UNDOPED POROUS ALUMINUM OXIDES AND NANOCOMPOSITE CeO2-ZrO2 AND Al2O3 CONTAINING MIXED OXIDES |
CN103619468A (en) * | 2011-07-01 | 2014-03-05 | 特莱巴赫工业有限公司 | Ceria zirconia alumina composition with enhanced thermal stability |
CN106732523A (en) * | 2017-02-21 | 2017-05-31 | 云南冶金集团创能金属燃料电池股份有限公司 | Catalyst carrier and preparation method |
CN106944031A (en) * | 2011-07-14 | 2017-07-14 | 特莱巴赫工业有限公司 | Cerium oxide zirconia alumina composition with enhanced heat endurance |
CN109395712A (en) * | 2018-12-07 | 2019-03-01 | 昆明冶金研究院 | A kind of aluminum-based catalyst agent carrier and preparation method thereof |
CN109513432A (en) * | 2018-12-07 | 2019-03-26 | 昆明冶金研究院 | A kind of catalyst carrier for purifying vehicle tail gas and preparation method thereof |
-
2019
- 2019-07-12 CN CN201910631862.7A patent/CN110282643A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090023581A1 (en) * | 2004-12-30 | 2009-01-22 | Magnesium Elektron Limited | THERMALLY STABLE DOPED AND UNDOPED POROUS ALUMINUM OXIDES AND NANOCOMPOSITE CeO2-ZrO2 AND Al2O3 CONTAINING MIXED OXIDES |
CN103619468A (en) * | 2011-07-01 | 2014-03-05 | 特莱巴赫工业有限公司 | Ceria zirconia alumina composition with enhanced thermal stability |
CN106944031A (en) * | 2011-07-14 | 2017-07-14 | 特莱巴赫工业有限公司 | Cerium oxide zirconia alumina composition with enhanced heat endurance |
CN106732523A (en) * | 2017-02-21 | 2017-05-31 | 云南冶金集团创能金属燃料电池股份有限公司 | Catalyst carrier and preparation method |
CN109395712A (en) * | 2018-12-07 | 2019-03-01 | 昆明冶金研究院 | A kind of aluminum-based catalyst agent carrier and preparation method thereof |
CN109513432A (en) * | 2018-12-07 | 2019-03-26 | 昆明冶金研究院 | A kind of catalyst carrier for purifying vehicle tail gas and preparation method thereof |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113337107A (en) * | 2021-05-29 | 2021-09-03 | 巢湖市龙鑫塑料有限公司 | Method for composite modification of nylon 6 by nano-alumina |
CN115228434A (en) * | 2022-07-21 | 2022-10-25 | 南京信息工程大学 | Surface-wrapped gamma-Al 2 O 3 : carbon nanotube adsorbent with Dy & lt 3+ & gt particles and preparation method thereof |
CN115228434B (en) * | 2022-07-21 | 2023-09-01 | 南京信息工程大学 | gamma-Al coated on surface 2 O 3 : dy3+ particle carbon nanotube adsorbent and preparation method thereof |
CN116332224A (en) * | 2023-03-22 | 2023-06-27 | 广东长信精密设备有限公司 | Spherical gallium oxide and preparation process thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101773830B (en) | High-temperature stability catalyst used for three-effect catalysis | |
CN103464152B (en) | Catalyst for tail gas purification and preparation method thereof | |
CN110282643A (en) | A kind of modified oxidized aluminum material and its preparation method and application | |
CN102716737A (en) | Preparation of Catalyst Supported by Cerium-Zirconium Solid Solution and Its Application in NOx Removal | |
CN101239313A (en) | Copper cerium aluminum catalyst and preparation method for simultaneously removing soot particles and nitrogen oxides | |
CN108479788B (en) | A kind of non-precious metal supported catalyst and its preparation method and use | |
CN106622380A (en) | Denitration catalyst and preparation method as well as application of denitration catalyst | |
CN101433831A (en) | Preparation of homogeneous mischcrystal cerium-zirconium-aluminum coating material by coprecipitation method and technique thereof | |
CN110354838A (en) | A kind of composite modified aluminium oxide of rare earth and its preparation method and application | |
CN105233814A (en) | Cerium oxide catalyst for catalyzing and purifying nitric oxides, preparation method and application | |
CN104383962A (en) | Base metal load type multistage pore zeolite molecular sieve catalyst of efficient catalytic combustion soot particles and preparation and application of catalyst | |
CN106621807B (en) | Flue gas treatment method for catalytic reduction, desulfurization and denitrification of titanium dioxide nanotube array loaded with lanthanum-cerium oxide | |
CN109277099B (en) | High-temperature hydrothermally stable SCR catalyst for diesel vehicle exhaust purification and preparation method thereof | |
JP4450763B2 (en) | Precious metal-containing composite metal oxide for exhaust gas purification catalyst and method for producing the same | |
CN103599768A (en) | Zirconium/lanthanum-modified gamma-alumina catalyst coating material and preparation method thereof | |
CN101428219B (en) | Oxynitride catalysis reductant in oxygen-enriched condition and preparation method thereof | |
CN112439406B (en) | Catalyst for catalytic oxidation of NO, and preparation method and application thereof | |
CN108212140A (en) | The high oxygen storage capacity Al of automotive catalyst2O3-CeO2-ZrO2-TiO2Coating material and preparation method thereof | |
CN103143347B (en) | Sulfur-tolerant oxidation catalyst and preparation method thereof | |
CN103611521A (en) | Barium-modified gamma-alumina catalyst coating material and preparation method thereof | |
CN103638917A (en) | Lanthanum-added modified gamma-alumina catalyst coating material and preparation method thereof | |
CN106824192A (en) | A kind of carbon-smoke combustion CuO catalyst of high activity and its preparation method and application | |
CN115805080B (en) | Low-temperature efficient green denitration catalyst and preparation method thereof | |
CN110548503A (en) | Cerium-based SCR denitration catalyst with wide temperature window and preparation method and application thereof | |
JP2006043683A (en) | Catalyst carrier, method for producing the same, and exhaust gas purification catalyst |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190927 |
|
RJ01 | Rejection of invention patent application after publication |